Tri-n-butyl phosphate(TBP)dissolved in kerosene was chosen as extractant for lithium from a modelbrine having high magnesium-to-lithium ratio and ferric chloride was added to the system.The influences of con-tact ti...Tri-n-butyl phosphate(TBP)dissolved in kerosene was chosen as extractant for lithium from a modelbrine having high magnesium-to-lithium ratio and ferric chloride was added to the system.The influences of con-tact time,concentration of the extractant,concentrations of some salts(Mg<sup>2+</sup>, Na<sup>+</sup>,K<sup>+</sup>)in the solution,acid-ity of hydrochloric acid and extraction temperature on the exttaction of lithium with TBP-kerosene system werestudied.The suitable extraction conditions were found to be:contact time not any less than 20min;at 20-25C;[Fe<sup>+3</sup>]/[Li<sup>+</sup>]about 1.5-2.0;TBP concentration 50%-70%;[MgCl<sub>2</sub>]exceeding 3 mol·L<sup>-1</sup>;pH about 2;while most sodium and potassium salts in the aqueous phase should be removed before the extraction.展开更多
文摘Tri-n-butyl phosphate(TBP)dissolved in kerosene was chosen as extractant for lithium from a modelbrine having high magnesium-to-lithium ratio and ferric chloride was added to the system.The influences of con-tact time,concentration of the extractant,concentrations of some salts(Mg<sup>2+</sup>, Na<sup>+</sup>,K<sup>+</sup>)in the solution,acid-ity of hydrochloric acid and extraction temperature on the exttaction of lithium with TBP-kerosene system werestudied.The suitable extraction conditions were found to be:contact time not any less than 20min;at 20-25C;[Fe<sup>+3</sup>]/[Li<sup>+</sup>]about 1.5-2.0;TBP concentration 50%-70%;[MgCl<sub>2</sub>]exceeding 3 mol·L<sup>-1</sup>;pH about 2;while most sodium and potassium salts in the aqueous phase should be removed before the extraction.